A method for pretreatment of molten iron desiliconization, dephosphorization, desulfurization and demanganization
A technology for pretreatment and molten iron, which is applied in the fields of dephosphorization, desulfurization, desiliconization of molten iron, and demanganese pretreatment, which can solve the problem that desiliconization and dephosphorization cannot be completed simultaneously.
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Embodiment 1
[0020] This embodiment focuses on desulfurization during the fourth stripping of molten iron, see Table 1 for details.
[0021] Table 1
[0022]
[0023] The specific calculation process is as follows:
[0024] The temperature of molten iron is 1250°C, the [Si] content is 0.426%, and the weight is 45.4 tons.
[0025] a. Oxygen is blown in until [Si] is fully oxidized and the exothermic temperature rises to 0.426×350=149°C; the oxygen consumption is 45.4×1000×0.426%×0.8=154.7m³;
[0026] b. The amount of lime added (the value of alkalinity is 1.5, the value of lime effective calcium oxide is 90%)=45.4×1000×0.426%×2.14×1.5 / 0.9=689.8kg, lime cooling=30×0.6898=20.7℃;
[0027] c. Amount of oxide scale added (12kg per ton of iron): 45.4×12=545.2kg; cooling down of oxide scale: 0.542×120=65.4;
[0028] d. The calculated temperature of the molten pool is: initial temperature + silicon element oxidation exotherm - lime cooling - oxide scale cooling = 1250+149-20.7-65.4 =1312.9°C;...
Embodiment 2
[0037] In this embodiment, the operations of dephosphorization and manganese removal are strengthened at the same time as the fourth removal of molten iron, see Table 2 for details.
[0038] Table 2
[0039]
[0040] The specific calculation process is as follows:
[0041] The temperature of molten iron is 1250°C, the content of [Si] is 0.44%, and the weight is 45.3 tons.
[0042] a. Oxygen is blown in until [Si] is fully oxidized and the exothermic temperature rises to 0.44×350=154°C; oxygen consumption is 45.3×1000×0.44%×0.8=159.5m³;
[0043] b. The amount of lime added (the value of alkalinity is 1.5, and the value of lime effective calcium oxide is 90%)=45.3×1000×0.44%×2.14×1.5 / 0.9= 711kg, lime cooling=30×0.711=21.3℃;
[0044] c. The amount of iron oxide scale added (the value is 22.5kg per ton of iron)=45.3×22.5=1008 kg; the temperature reduction of iron oxide scale=120×1.008=121°C;
[0045] d. The calculated temperature of the molten pool is: initial temperature + ...
Embodiment 3
[0054] In this embodiment, desulphurization is abandoned, and desiliconization, dephosphorization, and manganese removal are realized. The furnace number is 130000188 furnace times. See Table 3 for details.
[0055] table 3
[0056]
[0057] The specific calculation process is as follows:
[0058] The temperature of molten iron is 1250°C, the content of [Si] is 0.38%, and the weight is 44.6 tons.
[0059] a. Oxygen is blown in until [Si] is fully oxidized and the exothermic temperature rises to 0.38×350=133°C; oxygen consumption is 44.6×1000×0.38%×0.8=135.6m³;
[0060] b. The amount of lime added (due to abandoning desulfurization, single slag is used, the value of alkalinity is 2.5, and the value of lime effective calcium oxide is 90%)=44.6×1000×0.38%×2.14×2.5 / 0.9=1007kg, lime cooling=30 ×1.007=30.2℃;
[0061] c. Addition amount of iron oxide scale (23kg per ton of iron)=44.6×23=1026kg; cooling of iron oxide scale=120×1.026=123.1 ℃;
[0062] d. The calculated temperature...
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